Aziridine derivatives

ABSTRACT

An aziridine detergent-dispersant derivative, lube oil compositions containing said derivative, and manufacture thereof, said derivative being the reaction product of an aziridine of the formula:   WHERE R is hydrogen or omega -aminoalkyl of from 1 to 5 carbons and a monoethoxylated hydrolyzed polyalkene-P2S5 reactant, said derivative prepared by: A. FIRST CONTACTING AN ALIPHATIC POLYALKENE OF AN AVERAGE MOLECULAR WEIGHT OF BETWEEN ABOUT 50 AND 5,000 WITH P2S5 in the presence of sulfur at a first elevated temperature, B. SECOND CONTACTING THE RESULTING POLYALKENE-P2S5 reaction product with steam at a second elevated temperature, C. REMOVING INORGANIC PHOSPHORUS ACID FROM THE STEAM TREATED (HYDROLYZED) POLYALKENE-P2S5 reaction product, D. THIRD CONTACTING THE INORGANIC ACID FREE, STEAM TREATED POLYALKENE-P2S5 reaction product with ethylene oxide at a third elevated temperature in a mole ratio of said inorganic phosphorus acid free, steam treated P2S5-polyalkene reaction product to said ethylene oxide of between about 1:1 and 1:1.5 to form said monoethoxylated reactant, E. FOURTH CONTACTING THE ETHOXYLATED DERIVATIVE WITH SAID AZIRIDINE AT A FOURTH ELEVATED TEMPERATURE UTILIZING A MOLE RATIO OF SAID DERIVATIVE TO SAID AZIRIDINE OF BETWEEN ABOUT 3:1 AND 1:2 TO FORM SAID DETERGENT-DISPERSANT DERIVATIVE.

United States Patent [1 1 [111 3,865,810 Haugen et al. Feb. 11, 1975 AZIRIDINE DERIVATIVES CH 2-0.112 [75] Inventors: Haakon Haugen, Beacon; James G.

Dadura, Fishkill, both of NY.

[73] Assignee: Texaco Inc., New York, NY. R

[22] Filed: Sept. 14, 1972 where R is hydrogen or w-aminoalkyl of from I to 5 carbons and a monoethoxylated hydrolyzed polyalkene-P- S, reactant, said derivative prepared by:

a. first contacting an aliphatic polyalkene of an [21] Appl. No; 289,219

Related U.S. Application Data average molecular weight of between about 50 [62] Division of Ser. No. 143,185, May 13, 1971, Pat. No. and 5,000 with P 5 in the presence of sulfur at a 3,753,907. first elevated temperature,

b. second contacting the resulting polyalkene-P S, [52] U.S. Cl. 260/239 E, 260/260 EP, 260/128, reaction product with steam at a second elevated 252/32.7 HC, 252/467 temperature, [51] int. Cl C07d 23/06 c. removing inorganic phosphorus acid from the [58] Field of Search 260/239 E, 239 EP, 128; steam treated (hydrolyzed) polyalkene-P S Primary Examiner-Henry R. Jiles Assistant Examiner-Robert T. Bond Attorney, Agent, or Firm-T. H. Whaley; C. G. Ries ABSTRACT reaction product,

d. third contacting the inorganic acid free, steam treated polyalkene-P s reaction product with ethylene oxide at a third elevated temperature in a mole ratio of said inorganic phosphorus acid free, steam treated P S -polyalkene reaction product to said ethylene oxide of between about 1:1 and 1:1.5 to form said monoethoxylated reactant,

. fourth contacting the ethoxylated derivative with said aziridine at a fourth elevated temperature utilizing a mole ratio of said derivative to said aziridine of between about 3:1 and 1:2 to form said detergent-dispersant derivative,

12 Claims, N0 Drawings AZIRIDINE DERIVATIVES This is a division of application Ser. No. 143,185 filed May 13, 1971, now U.S. Pat. No. 3,753,907.

BACKGROUND OF INVENTION The trend towards high performance internal combustion engines and the introduction of emission control devices on motor vehicles have created a need for improved premium motor oils. Further, because of the ever increasing severity of the specifications of both the automobile manufacturers and the military, the modern crankcase lubricant must also have excellent diesel properties. To meet these demands for higher quality lubricants, new and improved additives are necessary. This need is particularly acute in the field of detergentdispersant additives. The detergent-dispersant additives function among other things to (l reduce sludge content of oils by maintaining formed sludge materials during engine operation in oil soluble dispersion, (2) reduce or inhibit the formation of varnish (resin) on engine surfaces and (3) inhibit the plugging of the positive crankcase ventilation (PCU) valve. In respect to the PCV valve if the valve becomes plugged or substantially plugged, the amount of sludge and resin precursors that are trapped in the crankcase will make effective lubrication very difficult. Although ashless dispersant such as the ethylene oxide derivative of an inorganic phosphorus acid free, steam hydrolyzed polyalkene-P S reaction product as taught in US. Pat. Nos. 3,087,956 and 3,272,744 have good sludge dispersion and resin and varnish inhibiting properties, it is only moderately effective in preventing the PCV valve from plugging.

SUMMARY OF INVENTION We have discovered and this constitutes our invention a new detergent-dispersant additive for hydrocarbon crankcase motor oils which has improved properties in respect to dispersing sludge, inhibiting varnish and resin build-up and is substantially superior in retarding the plugging of PCV valves. Another embodi ment of the invention is the manufacture of said additive and still another embodiment are crankcase lubricating oil compositions containing the novel additive.

More specifically, the invention pertains to a novel detergent-dispersant, manufacture and hydrocarbon lubricating compositions thereof, said dispersant being the reaction product of an aziridine characterized by the formula:

CH -CH where R is hydrogen or omega (w)-aminoalkyl of from 1 to 5 carbons and a monoethoxylated derivative of an inorganic acid dree, steam hydrolyzed polyalkene-P 8, reaction product.

DETAILED DESCRIPTION OF THE INVENTION In detail, the ashless detergent-dispersant additives of the invention are in essence a complex mixture of numerous individual compounds and are, therefore, characterized in terms of their method of preparation.

Specifically, the aziridine derivative of the monoethoxylated inorganic acid free, steam hydrolyzed P S reaction product is formed by first forming the inorganic phosphorus acid free, steam hydrolyzed polyalkene-P S precursor. This is accomplished by the reaction of P 5 (5-40 wt. percent of the reaction mass) with a polyalkene wherein the alkene monomer is from 2 to 5 carbons such as polyethylene, polypropylene, polybutylene, polyisobutylene, polypentylene having an average molecular weight between about 500 and 5,000. The reactions are conducted in the presence of between about 0.1 and 5 wt. percent sulfur at an elevated temperature of between about 100 and 320C, normally in a non-oxidizing atmosphere, for example, under a blanket of nitrogen, normally for a period of between about 1 and 10 hours. The reaction mixture if not in a liquid state is placed in a liquid state under preferred conditions. The liquefaction is accomplished by diluting the reaction mixture with a mineral lubricating oil having an SUS viscosity at 100F. between about 50 and 1,000. The lubricating oil usually constitutes between about 25 and wt. percent of the diluted reaction product concentrate.

The mineral oil diluted or undiluted polyalkene-BS reaction product is then hydrolyzed by contacting with steam desirably at a temperature between about and 260C. Under advantageous conditions, at least about one mole of steam per mole of reaction product is employed and the hydrolysis is normally conducted for a period of time of from 1 to 20 hours. The inorganic phosphorus acids formed during the hydrolysis are removed from the hydrolyzed reaction product prior to reaction with the ethylene oxide by standard procedures. A number of different removal procedures are available. In US. Pat. Nos. 2,951,835 and 2,987,512 removal is effected by contact with synthetic hydrous alkaline earth metal silicate and synthetic hydrous alkali metal silicates respectively. Inorganic phosphorus acids can also be removed by extraction with anhydrous methanol as disclosed in US. Pat. No. 3,135,729 which describes a process wherein organic phosphorus acids are eliminated from the hydrolyzed product by first drying the hydrolyzed product by passing inert gas such as nitrogen therethrough at between about and 200C. and then contacting the inorganic acids with anhydrous methanol under mixing conditions at a temperature between about 40 and 80C. in a methanol amount of between about 30 and 80 volume percent based on the overall mixture thereby forming an extract phase containing inorganic phosphorus acid and a mineral oil raffinate base containing inorganic phosphorus acid free, steam hydrolyzed ES -polyalkene reaction product. During the extraction procedure superatmospheric pressure may be applied, e.g., up to about 50 psig in order to maintain the methanol in the liquid state. At the end of the extraction step any methanol carried over into the raffinate phase is preferably removed, e.g., by stripping the raffinate with an inert gas such as nitrogen at an elevated temperature.

The inorganic phosphorus acid free hydrolyzed poly alkene-P 8 reaction product is then contacted with ethylene oxide in a mole ratio of oxide to reaction product of between about 1:1 and 1.5:1 at a temperature between about 60 and C, preferably at 80-125C., normally heating under reflux conditions for a period of time ranging from between about 0.5

and 2 hours, advantageously under pressures of from -500 psig. The reaction mixture is advantageously blown with an inert gas such as nitrogen at a temperature between about 100 and 125C. until the product is free of unreacted ethylene oxide.

lf desired, the ethylene oxide intermediate may have its odor reduced for better consumer acceptance of the final product. In said odor reduction nitrogen dioxide or a mixture of nitrogen dioxide and oxygen alternatively diluted with an inert gas such as nitrogen is contacted, e.g., bubbled through with a derivative at a temperature between about 65 and 150C. until at least about 0.15 wt. percent nitrogen dioxide, and preferably less than about 0.22 wt. percent nitrogen dioxide is absorbed by the derivative based on the weight of the derivative. Under advantageous conditions, nitrogen dioxide is diluted with air or an inert gas such as nitrogen, carbon dioxide and the like, containing about 1 volume percent or more of nitrogen dioxide. Advantageously, the reactive gas is introduced into the derivative at a rate of between about 0.001 to 0.5, preferably between about 0.01 and 0.02 standard cubic feet (SCF)/lb. of derivative per hour. The residual oxides of nitrogen are removed by stripping with a relatively inert gas such as nitrogen or air.

In the third final stage of the reaction, the monoethoxylated hydrolyzed-P 5 reaction product from the second stage is contacted, preferably in an inert atmosphere (e.g., nitrogen), with an aziridine characterized by the formula:

CH CH N I B where R is hydrogen or w-aminoalkyl of from 1 to 5 carbons, at a temperature between about and 130C, utilizing a mole ratio of reaction product to aziridine of between about 3:1 and 1:2, advantageously for a period of time between about 1 and 8 hours to form the desired aziridine derivative product of monoethoxylated inorganic phosphorus acid free, steam hydrolyzed polyalkene-P S reaction product.

Under preferred conditions, when w-aminoalkyl aziridine is employed the mole ratio is preferably about 1:1, when ethyleneimine is employed, the mole ratio is preferably between 2:1 and 1:2 for maximum desirable properties. Further, under preferred conditions, when the derivative is of an w-aminoalkyl aziridine, it is desirable to extract the final product with a mixture (e.g., weight ratio of from 1:3 to 3:1) ofa liquid alkane (e.g., pentane) and liquid alkanol (e.g., methanol) of less than 7 carbons normally at temperatures between 20 and 50C. recovering the purified derivative as extractant. This extraction improves the sludge inhibiting, resin inhibition and varnish inhibition properties of the derivative. No substantial incremental improvement is obtained with the extraction of the ethyleneimine derivative.

Specific examples of aziridine reactants contemplated herein are ethyleneimine, N-(Z-aminoethyl) aziridine, N-(3-aminopropyl) aziridine and N-(5- aminopentyl) aziridine.

In the lubricating oil compositions containing the aziridine derivatives of the invention, hydrocarbon mineral oil is employed as the base material such as paraffin base, naphthene base or mixed paraffin based distillate or residual oils. The lubricating mineral oil base generally has been subjected to solvent refining to improve its lubricity and viscosity-temperature relationship as well as solvent dewaxing to remove waxy components and improve the pour of the oil. Broadly speaking, a mineral lubricating oil having an SUS viscosity at 100F. between about 50 and 1,000 may be used in the formulation of the improved lubricants of this invention. Advantageously, the viscosity range falls between about and 300 SUS at F.

The aziridine derivatives of the invention are present in the mineral lubricating oil base in concentrations sufficient to impart detergent-dispersancy, varnish and resin formation inhibiting amounts. ln concentrations used in the formulation of the finished lubricant, the concentration of the derivative can be as high as 50 wt. percent. In finished lubricants the concentration of the additive falls between about 0.2 and 10 wt. percent and concentrations of between about 1 and 5 wt. percent are often employed.

The mineral lubricating oils containing the derivatives of the invention usually contain other additives designed to impart other desirable properties thereto, for example, V1 improvers such as polymethacrylates are normally included therein as are corrosion inhibitors and supplementary detergents. A widely used Vl improver is polymethacrylate having the general formula:

where R is an aliphatic radical of from 1 to 20 carbons,

-CH CH -N-CH methyl, ethyl, decyl and m is and 35,000.

Another commonly used supplementary lube oil additive is an alkaline earth metal alkylpheno'late. Barium nonyl phenolate, barium dodecylcresolate and calcium dodecylphenolate are examples of such detergents. These products which are well known detergent additives are usually present in the lubricating oil in a concentration between about 0.1 and 5 wt. percent.

$till another commonly used supplementary lube oil additive are detergents such as overbased calcium hydrocarbon sulfonate, overbased with calcium carbonate as disclosed in U.S. Pat. Nos. 3,027,325; 3,312,618 and 3,537,996. This additive is also normally present in an amount of 0.1 and 5 wt. percent.

An often used supplementary lube oil inhibitor and antioxidant is a divalent metal dialkyl dithiophosphate resulting from the neutralization ofa P s -alcohol reaction product with a divalent metal or divalent oxide. Barium and zinc dialkyl dithiophosphates are widely used oxidation and corrosion inhibitors. Metal dialkyl an integer between 600 dithiophosphates are usually present in the lubricant in concentrations between about 0.1 and 3 wt. percent. The following examples further illustrate the invention but are not to be taken as limitations thereof.

EXAMPLE 1 This example illustrates the preparation of the inorganic acid free, hydrolyzed po1ybutene P S precursor from which the monoethoxylated reactant is derived.

To 400 lbs. of polyisobutene of an average molecular weight of about 1,300 there is added 79.3 lbs. of P S and 4 lbs. of elemental sulfur. The reaction mixture is heated under a blanket of nitrogen at a temperature of 232C. for a period of 6 hours. At the end of the reaction period the resultant isobutene-P S reaction mixture is diluted with 620 lbs. of hydrocarbon mineral oil of an SUS viscosity of 100 at 100F. The resultant lube oil concentrate of the reaction mixture is hydrolyzed by bubbling steam therethrough at a temperature of 176C. The steam contact is continued for a period of about 10 hours at a steam rate of about 10 lbs. per hour.

To the 1,084 lbs. of steam hydrolyzed polyisobutene- P 8 reaction product there is added under mixing conditions 466 lbs. of anhydrous methanol at about 60C. for a period of about 6 hours in order to extract into the methanol phase any inorganic phosphorus acids formed during the previous steam hydrolysis step. At the end of the methanol treating period the mixture is allowed to settle and methanol phase is decanted therefrom leaving an oil raffinate ofa Neut. No. of about 20 containing an inorganic acid free, steam hydrolyzed polyisobutene (1,300 m.w.)-P S reaction product.

EXAMPLE 11 This example illustrates the preparation of the monoethoxylated derivative reactant of the inorganic acid free, steam hydrolyzed po1yalkene-P S precursor prepared in Example 1.

With 130 lbs. of the oil phase of the type prepared in Example 1 containing the inorganic acid free, steam hydrolyzed polyisobutene (-l300 m.w.)-P S reaction product there was reacted 20 lbs. of ethylene oxide in a 30 gallon stainless steel reactor.

Specifically, air was removed from the system by heating to 105C. while blowing with nitrogen and ethylene oxide was introduced into the system at a sufficient rate to maintain a gentle reflux. The nitrogen flow was reduced during the ethylene oxide additions. When rapid reflux of ethylene oxide was known, ethylene oxide addition was reduced and the reaction mixture allowed to reflux for approximately 2 hours to assure completion of the reaction. Excess ethylene oxide was then removed from the reaction mixture by increasing the nitrogen rate and blowing for 2 hours at a temperature of about 105C. followed by N blowing to an N0 dosage of 0.2 wt. percent. After about 2 hours of nitrogen blowing the product was cooled to room temperature and there was produced 129.8 lbs. of deodorized monoethoxylated intermediate derivative of the inorganic acid free, steam hydrolyzed polybutene (1,300 m.w.) P reaction product having the following analysis:

Test Result Neut. No. 3.6 Hydroxyl No. 18.2 Phosphorus 0.97 Sulfur 0.68

EXAMPLE m This example illustrates the preparation of the ethyleneimine derivative of the monoethoxylated derivative of the type produced in Example 11.

To 2,713 grams (1 mole) of monoethoxylated derivative of Example I] kept at 50C. under a blanket of nitrogen at atmospheric pressure there was added 43 grams (1 mole) of ethyleneimine dropwise. The mixture was heated to C. for 4 hours. The resultant product weighed 2,676 grams (97 percent of theory) and contained 0.28 percent nitrogen (calculated 0.5 wt. percent), 0.63 wt. percent sulfur (0.6 wt. percent theory), 1.01 wt. percent phosphorus (1.0 wt. percent theory) and had a total base number (TBN) of 7 (calculated 20) and a Neut. No. of 2.6 (calc. 0).

EXAMPLE IV This example illustrates the preparation of the N-(2- aminoethyl) aziridinyl derivative of the monoethoxylated reaction product of the type produced in Example 11.

To 3,250 grams (1.2 moles) of monoethoxylated reaction product of Example [I kept at 50C. under a blanket of nitrogen at atmospheric pressure there was added 105 grams 1.2 moles) of N-(Z-aminoethyl) aziridine dropwise. The mixture was heated to 130C. for 6 hours and then was extracted with 2.4 liters pentane and 1 liter methanol. The pentane soluble part was solvent stripped under reduced pressure to give 3,030 grams percent yield) of product containing 0.8 wt. percent nitrogen (1 wt. percent calculated), 0.69 wt. percent sulfur (0.6 theory), 0.97 wt. percent phosphorus (1.0 wt. percent theory) witha TBN of 14 (calculated 40) and a Neut. No. of 6.4 (calculated 0).

EXAMPLE V This further example illustrates the additive and method of the invention and comparative additives. Run 1 To 2800 grams (1 mole) of monoethoxylated derivative of Example 11 kept at 50C. under a blanket of nitrogen at atmospheric pressure there was added 86 grams (2.0 moles) of ethyleneimine dropwise. The mixture was heated to 80C. for 3 hours. The resultant product weighed 2,805 grams (97 percent of theory) and was identified as the ethyleneimine derivative of the monoethoxylated reaction product of Example I1. Run 2 Same procedure as Example 111, but smaller scale, i.e., 543 grams (0.2 mole) of monoethoxylated derivative of Example 11 was reacted with 8.6 grams (0.2 mole) ethyleneimine. The product weighed 525 grams percent of theory) and was identified as the ethyleneimine derivative of the monoethoxylated derivative of Example 11.

Run 3 The Run 2 product in an amount of 200 grams (0.07 mole) was extracted with a mixture of 400 mls. of pentane and mls. of methanol. The pentane soluble part was stripped under reduced pressure to give 184 grams (92 percent of theory) of extracted Run 2 product. Run 4 The Run 1 product in an amount of 2,904 grams was prepared and extracted with a mixture of 2,400 mls. of pentane and 1,000 mls. of methanol. The pentane soluble portion was stripped under reduced pressure to give 2,788 grams (96 percent of theory) of an extracted Run 1 product.

EXAMPLE vi This example illustrates the lubricating oil compositions suitable for automotive use containing the derivatives of the invention and the superior function of the derivatives of the invention in respect to detergent dispersancy inhibition of engine varnish, resin and plugging of the positive crankcase ventilation valve.

The base lubricating oil composition, hereinafter designated as Base Oil A, employed in the subsequent tests 5 consists of a refined paraffinic distillate oil of an sus 600 grams (2 moles) monoethoxyiated f' viscosity of about 130 at 100F. containing 0.35 wt. of Example I] k at 50 under a blanket of percent Ca in the form of calcium carbonate overbased trogen at f'? pressure w added grams (1 calcium alkylated benzene sulfonate (alkylated benmole) of ethyleneimine dropwise. The mixture was Zene of -450 012 wt percent Zinc as Zinc heated to 80 C. for Shows. The resultant product 3 h ]b r l dithiophosphate and 0.5 wt. h 8 grams (y'eld 9 Percent Q F and percent ofa copolymer of lauryl and stearyl methacrylwas identified as the ethyleneimine derivative of the me in approximately 4:| weight ratio in mineral 0 Example mohoethoxylated P (-l45 SUS at 100F.) in a copolymer to oil weight 6 ratio of 2:3.

To 280 grams mole) of mohocthoxylated A brief description of the tests employed are as foltive of Example [1 kept at 50C. under a blanket of nilows. trogen at atmospheric pressure there was added 18.0 Bench Sludge Test (3ST) ghams rholc) of N'Q'amimethyl) azindihe drop The procedure comprises introducing into a bottle wlse- The was heated to 130C for 3 hours the test oil composition, cetane, titanium oxide (6 wt. TWO hundred grams of this P were extracted h percent) in oil, the titanium being coated with resini- 400 Of p and of methaholtied hydrocarbon blowby. The mixture is heated and Pentahe Soluble P was Solvent pp under agitated for 24 hours and centrifuged. The results are dhced Pressure to give 181 g Parcel)t of reported in mm. sediment depth and is inversely related Y) 0f the N-(2- yl) aliridine derivative of the to the ability of the lubricant formulation to disperse mohoethoxylated Prodhct of Example the foreign material in the formulation. Values of about Run 7 3.5 to 2.5 mm sediment indicate little or no disper- TO 280 grams mole) of monoethoxylated defivasancy. Values of 2.5 to 1.8 indicate a substantial level tive of Example 11 kept at 2 Under a blanket of of dispersancy and values below 1.8 are only obtained trogen at atmospheric pressure there was added 27.0 for formulations of outstanding dispersancy. grams (0.3 moles) of N-(2-aminoethyl) aziridine. The Resin Inhibition Test (RIT) mixture was heated to 50C. for 1 hour and t0 procedufe is run combining test hyfor 3 hours- TWO hundred grams of this Product was drocarbon blowby and hydrocarbon lubricating oil. tracted with 400 mls. 0f pent ne flfi 125 of meth- The resultant mixture is heated at an elevated temperaanol. The pentane soluble part was solvent stripped ture, diluted with additional mineral oil and the Lumeunder reduced pressure to give 180 grams (yield 90.0 tron turbidity of the sample is measured. The results percent of theory) of N-(Z-aminoethyl) aziridine derivrange from 100 to 0 percent turbidity. A rating less ative of the monoethoxylated product of Example ll. than 40 is usually favorable. The weight ratio of test The additive products of the above runs were ana composition to engine blowby to diluent oil is about lyzed and the results are as follows: l:l.25:l.

Ford MS-VB TABLE I The procedure of this test is outlined in ASTM Spe- ANALYSIS OF ETHYLENElMlNE AND N-(Z-AMINOETHYL) 33 Techmca] Pubhcdnon N 3154: enhfled pingme AZIRIDNE DERIVATIVES OF EXAMPLE H PRODUCT est Sequences For Evaluating Automotive Lubricants Analysis For API Service MS. A sludge rating and varnish rating of 50 indicates a clean engine with decreasing val- WL P s N TBN ues indicating increasing sludge and varnish deposition. 1 0.87 057 0.82 m 12 The PCV valve rating given in percent of plugging 2 1.0 0.63 0.30 2.6 6 thereof 2 12 8:23 8:5; 3:3 The additives tested, whose results are reported 5 0.96 0.61 0.18 3.2 4 5 below in Tables 11 and III were essentially those pre- 7 3 8:53 8:23 3:; i1 pared in Examples 11, IV and V. Runs A, J, K and A are comparative.

TABLE 11 BENCH TEST EVALUATlON Ex. 11: Amine Additive Run Additive Mole Ratio Extracted BST RlT A Product 2.5' 50 Ex. 11 Reacted with: I B Ethyleneimine 2:1 No 1.0

(Run 5) TABLE 11 -('onlinucd BENCH TEST EVALUATION Ex. 11: Amine Additive Run Additive Mole Ratio Extracted BST RIT C Ethyleneimine 1:1 No 1.0

(Run 2) D Ethyleneimine 1:1 Yes 0.9 3

(Run 3) E Ethyleneimine 1:2 Yes 1.1 Clear (Run 4) F Ethyleneimine 1 :2 No 1.0 Clear (Run 1) G N-(Z-Aminoethyl) 1:1 No 2.5 17

Aziridine (Ex. IV H N-(Z-Aminoethyl) 1:1 Yes 1.0 6

Aziridine (Ex. IV Extracted) I N-(2'Aminoethy1) 1:2 Yes 1.6 27

Aziridine (Run 6) .l N-(Z-Aminoethyl) 1:3 Yes 2.5 11

- Aziridine (Run 7) K N-(2'Aminoethy1) 1:4 Yes 3.2 5

Aziridine (Run 7A) 1. Test blends contained 7.5 wt. 7r Additive in Base Oil A. 2. The additive extracted with a mixture of pcntzuie and methanol.

TABLE III EVALUATION IN THE FORD MS-VB ENGINE TEST OF LUBE COMPOSITIONS CONTAINING DERIVATIVE OF EXAMPLE II AND AZIRIDINE PCV Valve Run Additive Sludge Varnish Plugging A Ex. II Product 31.7 28.2 94 C N-(Z-Aminoethyl) 39.5 37.1 48

Aziridine Derivative of Ex. 11 Product (1:1 mole ratio) E Ethyleneimine 45.8 32.8 38

Derivative of Ex. 11 Prod.

(2:1 mole ratio) 3. The additives were blended in Butte Oil A In give a phosphorus content 010,075 wt. /r.

4. A rating of 50 is clean,

We claim:

1. A method of preparing an aziridine derivative comprising:

a. first contacting a polyalkene of an average molecular weight between about 500 and 5,000 derived from an alkene of from 2 to 5 carbons with P 8 in the presence of between about 0.1 and 5 wt. percent sulfur at a temperature between about 100 and 320C, P 8 comprising between about 5 and 40 wt. percent of the reaction mixture to form a po- 1yalkene-P S first reaction product,

b. second contacting the said polyalkene-P 8 first reaction product with steam at a temperature between about 100 and 260C, utilizing at least about a mole ratio excess of steam in respect to said polyalkene-P 8 first reaction product to form a steam hydrolyzed polyalkene-P 5 second reaction product,

. third removing inorganic phosphorus acid from the steam hydrolyzed polyalkene-P 8 second reaction product to form an inorganic phosphorus acid free, steam hydrolyzed polyalkene-P 8 third product,

d. fourth contacting said inorganic phosphorus acid free, steam hydrolyzed polyalkene-P 5 third prod uct with ethylene oxide in a mole ratio of reaction product to ethylene oxide of between about 1 and where R is hydrogen or w-aminoalkyl of from 1 to 5 carbons at a temperature between about 25 and C., utilizing a mole ratio of said fourth reaction product to aziridine of between about 3:1 and 1:2 to form said aziridine derivative.

2. A method in accordance with claim 1 wherein said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step e is about 1:1.

3. A method in accordance with claim 1 wherein said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step e is about 1:2.

4. A method in accordance with claim 1 wherein said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step e is about 2:1.

5. A method in accordance with claim 1 wherein said aziridine derivative is extracted from the final reaction mixture in step e with a mixture of liquid alkane and liquid alkanol of less than 7 carbons, said polyalkene is polyisobutene of a molecular weight of about 1,300 and said R is Z-aminoethyl and said mole ratio in step e is about 1:1.

6. A method in accordance with claim 1 wherein said aziridine derivative is extracted from the final reaction mixture in step e" with a mixture of liquid alkane and liquid alkanol of less than 7 carbons, said polyalkene is with claim 6. 

1. A METHOD OF PREPARING AN AZIRIDINE DERIVATIVE COMPRISING: A. FIRST CONTACTING A POLYALKENE OF AN AVERAGE MOLECULAR WEIGHT BETWEEN ABOUT 500 AND 5,000 DERIVED FROM AN ALKENE OF FROM 2 TO 5 CARBONS WITH P2S5 IN THE PRESENCE OF BETWEEN ABOUT 0.1 AND 5 WT. PERCENT SULFUR AT A TEMPERATURE BETWEEN ABOUT 100* AND 320*C., P2S5 COMPRISING BETWEEN ABOUT 5 TO 40 WT. PERCENT OF THE REACTION MIXTURE TO FORM A POLYALKENE-P2S5 FIRST REACTION B. SECOND CONTACTING THE SAID POLYALKENE-P2S5 FIRST RE C PRODUCT WITH STEAM AT A TEMPERATURE BETWEEN ABOUT 100* AND 260*C., UTILIZING AT LEAST ABOUT A MOLE RATIO EXCESS OF STEAM IN RESPECT TO SAID POLYALKENE-P2S5 FIRST REACTION PRODUCT TO FORM A STEAM HYDROLYZED POLYALKENE-P2S5 SECOND REACTION PRODUCT, C. THIRD REMOVING INORGANIC PHOSPHORUS ACID FROM THE STEAM HYDROLYZED POLYALKENE-P2S5 SECOND REACTION PRODUCT TO FORM AN INORGANIC PHOSPHORUS ACID FREE, STEAM HYDROLYZED POLYALKENE-P2S5 THIRD PRODUCT, D. FOURTH CONTACTING SAID INORGANIC PHOSPHORUS ACID FREE, STEAM HYDROLYZED POLYALKENE-P2S5 THIRD PRODUCT WITH ETHYLENE OXIDE IN A MOLE RATIO OF REACTION PRODUCT TO ETHYLENE OXIDE OF BETWEEN ABOUT 1 AND 4 AT A TEMPERATURE BETWEEN ABOUT 60 AND 150*C. UNDER A PRESSURE OF BETWEEN ABOUT 10 AND 500 PSIG TO FORM MONOETHOXYLATED INORGANIC PHOSPHORUS FREE, STEAM HYDROLYZED POLYALKENEP2S5 FOURTH REACTION PRODUCT, E. CONTACTING SAID FOURTH REACTION PRODUCT WITH AN AZIRIDINE CHARACTERIZED BY THE FORMULA:
 2. A method in accordance with claim 1 wherein said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step ''''e'''' is about 1:1.
 3. A method in accordance with claim 1 wherein said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step ''''e'''' is about 1:2.
 4. A method in accordance with claim 1 whereiN said polyalkene is polyisobutene of a molecular weight of about 1,300, said R is hydrogen and said mole ratio in step ''''e'''' is about 2:1.
 5. A method in accordance with claim 1 wherein said aziridine derivative is extracted from the final reaction mixture in step ''''e'''' with a mixture of liquid alkane and liquid alkanol of less than 7 carbons, said polyalkene is polyisobutene of a molecular weight of about 1,300 and said R is 2-aminoethyl and said mole ratio in step ''''e'''' is about 1:1.
 6. A method in accordance with claim 1 wherein said aziridine derivative is extracted from the final reaction mixture in step ''''e'''' with a mixture of liquid alkane and liquid alkanol of less than 7 carbons, said polyalkene is polyisobutene of a molecular weight of about 1,300 and said R is 2-aminoethyl and said mole ratio in step ''''e'''' is about 1:2.
 7. AN AZIRIDINE DERIVATIVE IN ACCORDANCE WITH CLAIM
 1. 8. An aziridine derivative prepared in accordance with claim
 2. 9. An aziridine derivative prepared in accordance with claim
 3. 10. An aziridine derivative prepared in accordance with claim
 4. 11. An aziridine derivative prepared in accordance with claim
 5. 12. An aziridine derivative prepared in accordance with claim
 6. 